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Kinetic theories for granular flow: inelastic particles in Couette flow and slightly inelastic particles in a general flowfield

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TLDR
In this paper, the authors studied the flow of an idealized granular material consisting of uniform smooth, but nelastic, spherical particles using statistical methods analogous to those used in the kinetic theory of gases.
Abstract
The flow of an idealized granular material consisting of uniform smooth, but nelastic, spherical particles is studied using statistical methods analogous to those used in the kinetic theory of gases. Two theories are developed: one for the Couette flow of particles having arbitrary coefficients of restitution (inelastic particles) and a second for the general flow of particles with coefficients of restitution near 1 (slightly inelastic particles). The study of inelastic particles in Couette flow follows the method of Savage & Jeffrey (1981) and uses an ad hoc distribution function to describe the collisions between particles. The results of this first analysis are compared with other theories of granular flow, with the Chapman-Enskog dense-gas theory, and with experiments. The theory agrees moderately well with experimental data and it is found that the asymptotic analysis of Jenkins & Savage (1983), which was developed for slightly inelastic particles, surprisingly gives results similar to the first theory even for highly inelastic particles. Therefore the ‘nearly elastic’ approximation is pursued as a second theory using an approach that is closer to the established methods of Chapman-Enskog gas theory. The new approach which determines the collisional distribution functions by a rational approximation scheme, is applicable to general flowfields, not just simple shear. It incorporates kinetic as well as collisional contributions to the constitutive equations for stress and energy flux and is thus appropriate for dilute as well as dense concentrations of solids. When the collisional contributions are dominant, it predicts stresses similar to the first analysis for the simple shear case.

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Fluid and Particle Coarsening of Drag Force for Discrete-Parcel Approach

TL;DR: In this article, the coarsening of the fluid and particle phases has been investigated in fine-grained Euler-Euler simulations of gas-fluidization of uniformly sized particles in three-dimensional periodic domains.
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Modeling of particle transport and combustion phenomena in a large-scale circulating fluidized bed boiler using a hybrid Euler–Lagrange approach

TL;DR: In this article, a hybrid Euler-Lagrange approach was used to model the dense gas-solid flow combined with a combustion process in a large-scale industrial CFB boiler.
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Advances in mathematical modeling of fluidized bed gasification

TL;DR: In this article, the authors investigated the different modeling approaches applied to the fluidized bed gasification systems and classified them as the equilibrium model and the rate-based or kinetic model, depending on the description of the hydrodynamic of the bed.
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Computational fluid dynamic (CFD) simulation of a pilot-scale annular bubble column photocatalytic reactor

TL;DR: The behavior of an 18-l pilot-scale photocatalytic reactor has been investigated using a computational fluid dynamic (CFD) approach and the granular Eulerian model was used to describe the multiphase flow system.
Journal ArticleDOI

Study of wall-to-bed heat transfer in a bubbling fluidised bed using the kinetic theory of granular flow

TL;DR: In this article, a two-fluid Eulerian-Eulerian model has been carried out applying the kinetic theory of granular flow (KTGF) to a wall-to-bed reactor and the local heat transfer coefficients are compared against experimental data for two drag models, namely the Gidaspow and the Syamlal-O'Brien drag models.
References
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Journal ArticleDOI

Equation of State for Nonattracting Rigid Spheres

TL;DR: In this paper, a new equation of state for rigid spheres has been developed from an analysis of the reduced virial series, which possesses superior ability to describe rigid-sphere behavior compared with existing equations.
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Experiments on a Gravity-Free Dispersion of Large Solid Spheres in a Newtonian Fluid under Shear

TL;DR: In this article, a large number of spherical grains of diameter D = 0.13 cm were sheared in Newtonian fluids of varying viscosity (water and a glycerine-water-alcohol mixture) in the annular space between two concentric drums.
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